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111.
General equations for emittance and reflectance of multilayer systems are given. It is demonstrated that band distortions can be avoided by application of the appropriate working equations. An opaque (thick) sample is employed as a reference. 相似文献
112.
FTIR reflection spectra of molten chloroaluminates containing alkali earth chlorides showC
2v
andC
3v
perturbations of AlCl
4
–
. The splitting ofv
3(F
2) is proportional to the ionic potential of the counterion. The observation of anion-cation stretching vibrations allows the strength of the interaction to be evaluated. Molten NaAl2OCl5 is assumed to contain the Al4O2C1
10
2–
ion. 相似文献
113.
Displacement of oil trapped in water-wet reservoirs was analyzed using percolation theory. The critical capillary number of the CDC (Capillary Desaturation Curve) was be predicted based on the pore structure of the medium. The mobilization and stability theories proposed by Stegemeier were used to correlate oil cluster length to the capillary number needed to mobilize the trapped oil. Under the assumption that all pore chambers have the same size, a procedure was developed using the drainage capillary pressure curve and effective accessibility function to predict the CDC curve for a given medium. The prediction of critical capillary numbers was compared with the experimental data from 32 sandstone samples by Chatzis and Morrow. Also, the CDC curve of one sandstone sample was calculated using the procedure developed in this work and compared with the measured data. Very good agreements were obtained.Nomenclature
a
average radius of a liquid filament [m]
-
c
constant
-
D
pore throat diameter [m]
-
D
a
advancing diameter of an oil cluster [m]
-
D
af
average flowing diameter of the medium [m]
-
D
da
controlling diameter of the medium [m]
-
D
r
receding diameter of an oil cluster [m]
-
D
X
difficulty index
-
f
ratio of length to average radius of an oil cluster
-
F
i
interfacial forces [N]
-
F
p
force from pressure gradient [N]
-
g
wettability function
-
k
absolute permeability [m2]
-
l
length of an oil cluster [m]
-
l
m
mobile oil cluster length [m]
-
l
s
stable oil cluster length [m]
-
l
w
wavelength [m]
-
n*
relative length of an oil cluster
-
N
c
1
capillary number defined by Equation (1)
-
N
c
2
capillary number defined by Equation (2)
-
P
b
probability of oil filling a pore
-
P
c
percolation threshold value
-
p
c
capillary pressure [N/m2]
-
r
radius of a pore [m]
-
r
e
average pore radius [m]
-
S
n
the nonwetting phase saturation
-
S
or
residual oil saturation
-
S
orn
normalized oil saturation
-
v
Darcy flow rate [m/s]
-
X
t
total fraction of pores
-
X
t
a
accessibility
-
X
e
a
effective accessibility
-
(D)
pore throat size distribution function
-
a
advancing contact angle
-
r
receding contact angle
-
porosity
-
density of the liquid [kg/m3]
-
constant in Equation (4)
-
dynamic length of an oil cluster [m]
-
interfacial tension [N/m]
-
viscosity [N/(m s)]
- p
pressure gradient [N/m3] 相似文献
114.
A Computational Study of the Homogeneous Algorithm for Large-scale Convex Optimization 总被引:3,自引:0,他引:3
Recently the authors have proposed a homogeneous and self-dual algorithm for solving the monotone complementarity problem (MCP) [5]. The algorithm is a single phase interior-point type method; nevertheless, it yields either an approximate optimal solution or detects a possible infeasibility of the problem. In this paper we specialize the algorithm to the solution of general smooth convex optimization problems, which also possess nonlinear inequality constraints and free variables. We discuss an implementation of the algorithm for large-scale sparse convex optimization. Moreover, we present computational results for solving quadratically constrained quadratic programming and geometric programming problems, where some of the problems contain more than 100,000 constraints and variables. The results indicate that the proposed algorithm is also practically efficient. 相似文献
115.
116.
Ingvild Bruaseth Matthias Bahr Dirk Gerhard Erling Rytter 《Journal of polymer science. Part A, Polymer chemistry》2005,43(12):2584-2597
Ethene homopolymerizations and copolymerizations with 1‐hexene were catalyzed by methylaluminoxane‐activated (1,2,4‐Me3Cp)2ZrCl2. Investigations of the effects of various pressures on the homopolymerizations and copolymerizations and of the effects of different concentrations of trimethylaluminum (TMA) on the copolymerizations were performed. The characteristics of the ethene/1‐hexene copolymers agreed with expectations for changes in the ethene concentration: the incorporation of 1‐hexene decreased, whereas the melting point and crystallinity increased, with increasing pressure. The main termination mechanism of the homopolymerizations was β‐hydrogen transfer to the monomer. Termination mechanisms resulting in vinylidene unsaturations dominated in the copolymerizations. Standard termination mechanisms producing vinyl and trans‐vinylene unsaturations occurred in parallel and were not influenced by the ethene or TMA concentration. In addition, some chain transfer to TMA, producing saturated end groups after hydrolysis, occurred. Copolymerizations with different additions of TMA, with the other polymerization conditions kept constant, showed that the catalytic productivity [tons of polyethylene/(mol of Zr h)], the 1‐hexene incorporation, and the molecular weight (from gel permeation chromatography) were independent of the TMA concentration. Surprisingly, the vinylidene content decreased almost linearly with increasing TMA concentration. TMA might have coordinated to the catalytic site after 1‐hexene insertion and rotation to the β‐agostic state and, therefore, suppressed the standard termination reactions after 1‐hexene insertion. © 2005 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 43: 2584–2597, 2005 相似文献
117.
Vinyl chloride was polymerized at 40–96% of saturation pressure in water suspended systems at 55°C with suspension PVC as a seed. The monomer was continuously charged as vapor from a storage vessel kept at lower temperature. Characterization included molecular weight distribution (MWD) and degree of long-chain branching (LCB) by GPC and viscometry, thermal dehydrochlorination, microscopy, and technical standard tests. A granular seed was necessary to obtain granular polymer and reasonable polymerization rate. In properly seeded systems with monomer-soluble initiator, crust formation is very low. With monomer-soluble initiator the polymerization reactions are restricted to the seed polymer, comprise its total structure, reducing its porosity. At pressure near saturation, molecular weight increased with conversion, and autoacceleration occurred. The changes in molecular weight are presumably due to the lack of a liquid monomer phase, which reduces the mobility of the radicals leading to decreased termination. At decreasing polymerization pressure the mobility is further reduced due to de-swelling of the gel. At low pressure the polymerization rate decreased, the amount of low molecular weight material increased, and considerable long-chain branching occurred as a result of monomer depletion. With water-soluble initiator (at pressure near saturation), new tiny particles were formed in the water phase at the boundary to the seed particles. The seed structure remained unchanged. The polymer formed showed broad MWD and high LCB. No marked reduction in polymerization rate was observed. The dehydrochlorinatlon measurements indicate that the end groups and not the branch points are responsible for the decrease in thermal stability noticed. 相似文献
118.
Martin Ystenes Jan L. Eilertsen Jianke Liu Matthias Ott Erling Rytter Jon A. Stvneng 《Journal of polymer science. Part A, Polymer chemistry》2000,38(17):3106-3127
The structure of methylaluminoxane (MAO), used as a cocatalyst for olefin polymerization, has been investigated by Raman and in situ IR spectroscopy, polymerization experiments, and density functional calculations. From experimental results, a number of quantum chemical calculations, and bonding properties of related compounds, we have suggested a few Me18Al12O9 cage structures, including a highly regular one with C3h symmetry, which may serve as models for methylaluminoxane solutions. The cages themselves are rigid but may contain up to three bridging methyl groups on the cage surfaces that are labile and reactive. Bridging methyls were substituted with Cl atoms to form a compound otherwise similar to MAO. Chlorinated MAO is unable to activate a metallocene catalyst, even in the presence of trimethylaluminum (TMA), but allows subsequent activation by regular MAO. With bis(pentamethylcyclopentadienyl)zirconium dichloride, MAO and TMA seem to influence chain termination independently. Several findings previously poorly explained are rationalized with the new model, including the observed lack of reaction products with excess TMA. © 2000 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 38: 3106–3127, 2000 相似文献
119.
Hanne Wigum Linda Tangen Jon Andreas Stvneng Erling Rytter 《Journal of polymer science. Part A, Polymer chemistry》2000,38(17):3161-3172
Ethene homopolymerization and copolymerization with 1‐hexene were catalyzed by methyl‐substituted cyclopentadienyl (Cp) zirconium dichlorides, (Rn C5H5−n)2ZrCl2 (Rn = H, Me, 1,2‐Me2, 1,3‐Me2, 1,2,3‐Me3, 1,2,4‐Me3, Me4, or Me5), and methylaluminoxane. The polymers were characterized with Fourier transform infrared, nuclear magnetic resonance, gel permeation chromatography, and differential scanning calorimetry techniques. Generally, an increasing number of methyl substituents on the Cp ligand results in lower 1‐hexene incorporation in the copolymer. The two catalysts with split methyl substitution (Rn = 1,3‐Me2 and Rn = 1,2,4‐Me3) show a higher comonomer response than their disubstituted and trisubstituted counterparts (Rn = 1,2‐Me2 and Rn = 1,2,3‐Me3). They even incorporate more 1‐hexene than Rn = H and Rn = Me. These findings are qualitatively in agreement with the results of a theoretical study based on density functional calculations. The presence of comonomer does not influence the termination reactions after the insertion of ethene. There is more frequent termination after each hexene insertion with increasing comonomer incorporation except for the two catalysts with split methyl substituents. The termination probability per inserted comonomer is highest for the less substituted catalysts. © 2000 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 38: 3161–3172, 2000 相似文献
120.